Heat exchange system



Feb. 21, 1939. H, G. MOJONNIER HEAT EXCHANGE SYSTEM Filed May 2, 1938 2 Sheets-Sheet l NSN Feb. 21, 1939. H. G. MoJoNNlER l 2,147,912

HEAT EXCHANGE SYSTEM Filed May 2, 1933 2 sheets-sheet 2 l l i n 76 magy Patented Feb. 21, `1939 UNITED STATESA PATENT oFFlcE HEAT EXCHANGE SYSTEM Harry G. Mojonnier, Oak Park, Ill., assigner to Mojonnier Bros. Co., a corporation o! Illinois Application May 2, 193s, serial No. 205,425

5 Claims.

The present invention relates to heat exchange systems and has to do more particularly with the control of the temperature in the heat exchange elements.

The principal object of the invention is to provide a system of the kind mentioned wherein the temperature of the heat exchange medium within the heat exchange elements will be changed in accordance with.certain changes in the rate of ow of the liquid being treated.

The invention has been developed in connection with the heat treatment of milk and milk products and accordingly will be so described, although it will be apparent that the same may be used in the treatment of other liquids.

As illustrative, we may consider the application of the invention to the efcient cooling of milk with ammonia as the refrigerant. While the milk is owing over the cooling elements of the exchanger, it is desirable to maintain the ammonia which is in liquid form as it enters the heat exchange elements, at a temperature of about 28 degrees Fahrenheit. This is below the freezing point. Hence, if no provision be made to meet-the objection, 'as soon as the ow of milk falls off or stops, the milk will freeze on the cooling elements. Then when the milk :Elow 'starts up again, the ice formed on the elements will act as an insulator and therefore satisfactory cooling is impossible. l3nt by the use of the present invention this freezing will be avoided. A selective regulator lis used to change the ammonia temperature .from a freezing one to a non-freezing one. Ordinarily this isa change from 28 degrees Fahrenheit to 34 degrees Fahrenheit. This change is made in accordance with the milk flow. A heavy flow brings on the low temperature and a falling oit or stopping of the flow brings on the high temperature.

More specifically stated, I employ a back pressure regulator having two diaphragms and these are brought into play, the one or the other, as the milk flow changes from heavy to light, or vice versa. The diaphragms are subjected to pressure in the suction side o the system, and thus by maintaining one pressure or the other, the corresponding and desired temperatures result. A perforated tray or pan is located in the path of travel of the treated milk, and is used to bring about proper operation of the regulator. When a full flow of milk is on, the pan is pressed down by the milk stream and occupies one operative position. When the llow is light or partial,

the milk will pass through the periorations of the pan fast enough so that it will not accumulate in the pan, and therefore the pan will not be moved downward. Hence, in this condition of flow, the pan remains elevated and this is the second operative position of the pan. One operative position corresponds to the high pres- (Cl. (i2-141) sure of ammonia gas, while the other corresponds to the low pressure of ammonia gas, the former producing the higher temperature and the latter the lower temperature.

For a full understanding of the invention reference should be had to the following detailed description taken in connection with the accompanying drawings, while the scope of the invention will be particularly pointed out in the appended claims.

In said drawings, Fig. 1 is a diagram of a vheat exchange system designed for cooling milk by the use of ammonia, in what is called a gravity controlled system, the parts being constructed and arranged in accordance with the present invention. Fig. 2 is a central vertical section of a regulator used in the control of the ammonia gas pressure, and, hence, in the control of the heatl exchanger temperature. Fig. 3 is a side elevation of a portion of a heat exchanger, illustrating particularly the pan in the path of travel of the milk as it leaves the exchange elements, the same operating to control the regulator. And Fig. 4 is a horizontal section through the structure of Fig. 3, illustrating particularly the extent of the pan and its location relative to the exchange elements, the plane of section being indicated by the line ll---d of Fig. 3. Throughout these views like characters refer to like parts.

Upon a consideration of the diagram of Fig. 1, A designates the heat exchanger; B, the surge tank which receives the ammonia; C, the regulator by which the pressure in the tank is conthe milk flow to actuate the regulator C.

'I'he heat exchange elements l0 of the heat exchanger A are of well known construction, being in general like those illustrated and described in the UnitedStates Patent No. 2,040,947, granted May 19, 1936, to O. W. Mojonnier et al. Each element is made up of constituent plates Il which are pressed into shape to provide interior passages for the ow of the controlling medium, whether the same be ammonia, brine, chilled water, or otherwise, for cooling; or steam, hot water, or otherwise, for heating. By referring to the heat exchange element I0, shown in Fig. 3, it will be seen that from an intake pipe l2, two parallel passages I3 extend to the right, where they communicate with an end passage i4, and the latter through two parallel passages I5 communicates with an end passage Il at the left. The remainder of the path of travel through the heat exchange element under consideration,

the element through the outlet pipe I8. In the cov aforesaid Patent No. 2,040,947, the elements are provided with hinges and tubular hose connections. In this instance, each of the intake and outlet pipes I2 and |8 is provided with a hollow hinge |9. A flanged union nut 20 unites the hinge I9 to the element terminal in each case. In a similar way the lower end of the hinge is connected to the associated manifold 2| by a suitable stuiling box connection 22. In this way each of the elements I is free to rotate upon its mated hinges I9, the one connected with the lower manifold 2| and the other with the upper manifold 23. As shown in Fig. 4, there are four heat exchange elements l0 and the manifolds are arranged for two extra elements in case they are required. As shown in the case of manifold 2|, the openings for the hinges required by these extra elements are closed by suitable plugs 24. The manifold 2| has a laterally extending central tubular portion 25, and into the outer threaded end of this portion is threaded the intake pipe 26. In a similar way. the manifold 23 is provided with a central portion connected to outlet pipe 21.

The manifolds 2| and 23 are connected to uprights 28 and 29 of the exchanger frame. The arrangement of these manifolds relative to `the frame members can be completely understood from a consideration of the manifold 2| which is fully illustrated. Obviously, the heat exchange medium coming in through pipe 26 will pass through the several hinges I9 and the associated exchange elements I I and out through the corresponding outlets I8 and associated hinges in' parallel into manifold 23 and from that point through pipe 21 on to the surge tank B. The elements I0 have their inner and outer ends turned laterally to form strengthening flanges 30 and 3|. When in service the heat exchange elements I0 are spaced apart by a distributor 32 indicated in the diagram of Fig. 1. This distributor rests upon the upper edges of the elements IIJ, all as shown more particularly in the aforesaid Patent No. 2,040,947. When'it is desired to clean the elements Ill, the distributor 32 is' removed and the elements swung apart on their hinges I9.

After cleaning, they are returned to normal op' erating position andv the distributor 32 is put back in place. Y

The frame members 28 and 2 9 are suitably secured together at ltheir upper ends while at their lower ends they are secured respectively to side frame members 33 and 34 which lie horizontally and are welded to the side members 36 and 31 of K a receiving pan 35 which is positioned directly below the elements I0 and extends far enough to catch all the liquid which falls from them. The receiving pan 35 has a front wall 38, a rear wall 39 and a bottom 40, besides the side walls 36 and 31. The bottom 40 is depressed slightly at 4I to form a trough for the collection of residual liquid and the guidingofthe same to the outlet pipe 42, which is suitably threaded at 43 for a pipe connection. Thus, in operation the collected liquid is continuously carried off through a suitable discharge pipe. Ordinarily, in service the exchange elements I0 are inclosedwithin cabinet doors but these neednot be disclosed herein. Reference may be had to the aforesaid Patent No. 2,040,947 for an illustration and description of these. The bottom of the exchanger A is provided with four legs 44 having ball feet 45.

` employing ammoniaas a refrigerant, and the control is what is called a gravity control.l yIn to a piston 64.

uid ammonia therein, the level of the latter being' indicated at |I.l 'Ihe change in the condition of the'ammonia as it travels up through the elements l0 is the result of its taking up heat from the liquid being treated, namely, the milk which flows down over the elements.

' The main valve of the controller C is positioned in the suction line made up of pipes 5| and 52, pipe 5| extending from the upper portion of tank B through to the intake side of the controller, and pipe 52 passing from the outlet side of the same on to the compressor D. A feeler pipe 53 extends from the upper portion of the surge tank B to the upper portion of controller C. 'I'he controller is one of well known construction, and is what is known to the trade as a dual-pressure, back-pressure valve or regulator. The main por-v tion of the regulator includes a b ody 54 divided by a partition 55 which is provided with a central aperture 56. Surrounding this aperture on the under side of the partition is an annular rib or bead 49, which constitutes the seat 'of the valve. The cooperating movable member is the valve member 51. 58 formed at the,low'er end of stem 59, -ashell 60 having its upper end threaded upon the head 56, and a cushion 6I seated between the upper end of the shell 60 and the head 58. The shell is cylindrical and is movably guided within the cylindrical walls of a guiding cap 62 threaded into a suitable opening in the valve body 54. A

coiled compression spring 63 serves, when unhin' gaging the seat 49.

'I'he upper end of the valve stem 59 is secured 'Ihis stem extends through a guiding sleeve 65 formed at the center of a web 66 which is secured in place as illustrated. This web has a plurality of openings 61 which extend completely through it, and thus place the space on the under side of the piston 64 in permanent communication at all times with the interior of the outlet pipe 52. 'I'he piston 64 is mounted to reciprocate in the bore of a cylinder 68 which is secured to Ythe upper side of the body 54 of the valve. The upper en d of the cylinder 68 is closed by an end 69 except for a central aperture 10. The structure is such that pressure on the upper side of the piston 64 will push it downward against the compressionof the spring 6|, and, upon `removal of the pressure above the piston, the spring willrestore the Ivalve to its closed position. -v i In order to get the necessary pressure on the upper side ofthe piston A64, suitable passages are provided from the feeler pipe. 5 3. These are all located, together vwith .the controlling Valves, within an upper casing 14 lwhich is secured at its lower end to the upper portion of the cylinder 68 in any suitable way. Within the casing 14 there are a number of passages which are arranged to bring the spring pressed diaphragm 15 at the left, as the parts are viewed in Fig. 2, or the spring-pressed diaphragm 16, at the right in the same figure, into service. The diaphragm 15 normally closes the upper end of a tubular valve seat 11. In like manner diaphragm 16 normally closes the upper end of a similar tubular valve seat 18. As clearly shown, the open lower end of tube 11 communicates through passage 19 with the chamber 88, which is in direct communication through passage 10 with the space on the upper side of the piston .64. Similarly, the lower end of the tubular valve seat 18 is in direct communication through a passage 8| with the same space 88.

i In addition to these passages, the space 82 on the under side of the diaphragm 15 is in direct communication with the interior of the feeler pipe 5,3. This space 8,2, as clearly shown, extends all the way around the tubular valve seat 11. The space 82 is in direct communication through passages 83 and 84, with a space 85 directly above and adjacent to the upper end of a tubular valve seat 86, located in the casing 14 about midway between the diaphragms 15 and 16. The valve seat 86 is normally closed by a bearing member or cushion 81 at the lower end of the solenoid coreV 88. When this core is raised so as to open the valve then space,85 is in direct communication with chamber 89. The latter chamber is also in communication through passage 98, with space 9| on the under side ,ofA diaphragm 16.

On the upper sideof diaphragm 15 is a cup-V shaped piston 92 which is normally pressed down against the diaphragm 15 by a compression spring 93. This spring rests at its lower end Within the cup of the piston 92, and at its upper end, it engages the flange of a head 94, which may be forced downward by an adjusting screw 95, threaded into,a suitable opening in the end 96 of that portion of the casing 14 whichlincloses the piston`92- There the cup-shaped piston 91 cooperates with a spring 98 andthe latter, through head 99 and Vscrew |88, may be used tobring aboutl proper pressure upon thediaphragm, the screw |88 being threaded into the end |8| of that portion of the casing 14 that includes the. piston 91 and its spring 98.

Above the heads 96 and |8| of the casing isaI solenoid winding or coil |82. Electric conductors |83 and |84 lead from its terminals to a suitable source of current. When the coil |82 is energized, the core 88 is raised to open the valve i81. When the coil |82 is deenergized, then the core 88 falls under the action of gravity and thereby closes valve 81. As we shall see moreV fully' hereinafter, the coil |82 is electrically under the control ofl the pan H.

Now, with reference to the operation of the controller C, it will be noted that, when the solenoid core 88 is down and Valve 81 is closed, then the diaphragm 15 at the left, as the parts are viewed in Fig. 2, will be available for service, but the diaphragm 16 will not be available for service. It is diaphragm 15 that will operate under the high pressure and diaphragm 16 that will operate under the low pressure. Whe'n`diaphragm 16 is to be used then the solenoid valve 81 must be open. When it is closed then only diaphragm 15 is available. The spring 93 is preferably heavier than thespring 98.in o'rder to suit the diaphragm 16 to" the heavier pressure-and the diaphragm 16 to the lighter pressure.

Now, if it be assumed that the ammonia gas within the surge tank B and feeler pipe 53 can only pass as far as diaphragm 15 and cannot reach diaphragm 16, then the pressure maintained in the tank B will be the high pressure. Thus, for example, the spring 93 may be set to hold the gas pressure at, say, 50 pounds persquare inch. When so set, then, obviously, any increase of gas pressurebeyond the 50 pounds, will cause diaphragm 15 to rise and gas under the increased pressure will pass through tube 11, passage 19, chamber 88, and passage 18 to the upper side of the piston 64.' Under these circumstances, the spring 63, which opposes the pressure of piston 68, is such as to present a less opposing force' than that applied by the piston. As a result, the valve 51 will bev opened and the gas in the upper part of tank B will pass at once through pipes 5| and 52, which pipes constitute the suction` line to the intake of the compressor D. This will cause the pressure in the tank B and the feeler pipe' 53 to fall away. When it has been lowered suiiciently, then diaphragm 15 will come into contact with seat 11 and shut o the further supply of high pressure gas to the piston 64. The spring 6| will thereupon return the valve 51 to its seat. This action will take place automatically over and over again whenever the pressures change sufliciently.` Thus, with the diaphragm 15 in'V service,'the pressure of the gasied ammonia in the tank B and the upper portions of the elements I8, under the assumed setting of the spring 93, will be kept at approximately 50 pounds per square nch. ,In practice it has been found that this pressureKgives a temperature of about 36 degrees Fahrenheit in the coldestfpor tions of the cooling elements.

Again, if it be assumed that the solenoid core 88 is raised, then, as before noted, the' interior of the feeler pipe will be in direct communication with space 9| on the under side of the diaphragm 16. This path may be traced from feeler pipe 53 through space 82, passages 83 andl 84, chamber 85, the interior of valve tube 86, chamber 89, and passage 98, to the space 9| below the diaphragm 16. With this communication open betweenthe feeler pipe 53 and the under side of diaphragm '16, and a lower pressure available for the control of the main valve 51, .itis clear that the lower pressure willnot raise the diaphragm 15 against the pressure of the stronger spring 93 and so there will be no communicating passage through-valve tube 11 and passage 19, as before. A

Now, in operation, the lower pressure being available in the gas supplied to the under side of the diaphragm 16, it will be clear that there WillA be a rising and falling of this diaphragm in the manner previously described in connection with the diaphragm 15, whenever the pressure in the surge tank B varies slightly from that for which the spring 98 of the piston '91 is set. In such operation the diaphragm 16 will open the passage from chamber 9| through the tubular seat 18 and passage 8| to the chamber 88, and thus to the upper side of the piston 64, causing'its operation in the manner previously describedin connection with the diaphragm 15. It will be borne in mind that the spring 6| is relatively weak and will not interfere with the operationof the valve 51 under diaphragm 16. As illustrative, the pressure for l which the spring 98 may be set may be assumed the less pressure availablein the operation of the I to be 43 pounds per square inch. When so set,

diaphragm 16 keeps the gas pressure in the tank elements I0.

Thus, with the diaphragm 16 in service,A the r` lower freezing temperature Will be used with the heavy ilows of milk over the elements. And this condition must prevail as long as the solenoid coil 02 is energized. But should the solenoid be deenergized, then diaphragm 15 will come into ,play, and then only the higher pressure of say, 50

pounds, will result, with the corresponding temperature of about 36 degrees, a condition desired when the light flows of milk over the elements I occur.

,K PThus, it will be seen from what has been said that the regulator C provides a dual control, each according to a given pressure. Itwill also be obvious that the different pressures correspond to different temperatures in the exchange elements I0, as before stated. Thus, if the diaphragm 16 be in use, then the exchanger A may be run at full capacity with a heavy flow of liquid over the elements. On the other hand, when the ilow drops oif, then the diaphragm is brought into play and the higher pressure at which the gasified ammonia is kept maintains a higher temperature in the elements I0.

`When it comes to the compressor D, the same is of usual construction and draws in the gasiiied ammonia through suction line 5|, 52 andcompresses the same, and passes it in compressed condition out through pipe |03 to the intake of the condenser E. As shown, the compressor D is driven by an electric motor |04' operating through a. belt |05 and receiving electric current through conductors |06 and |01. The circuit of the motor may be controlled in any desired way.

The condenser E is shown as comprising a series of coils |08 through which the compressed gasied ammonia is passed into a receiver F. As the compressed gas passes through these coils, cooling water from a supply pipe H0 passes down over the coils and as a-fresult the compressed gas is liquefied and passes into the receiver F in liquid form. 'A basin ||2 is indicated beneath the coils |08 and serves to collect the water which passes down over them. From this basin a pipe I3 leads to some suitable discharge point.

The liquid ammonia passes from the receiver F up through the pipe H4 to the float control valve G, associated with lthe surge tank B. 'Ihe pipe I I4, as shown, enters the lowerf portion of the valve G and the latter is connected by a short pipe H5 with a lower portion of the tank B. As before stated, the liquid ammonia in the tank B is at a denite height indicated by the line 50. As the level of this liquid may fall, valve G is opened to allow the passage of more liquid into the tank B. The iloat control includes a float H6 on the free end of an arm ||1 which is pivoted at 8, and, by means of anoperating arm H9, pressas down on a plunger to close the valve whenever the float H6 rises. When the oat I6 falls, then the plunger 20 moves in the opposite direction to open the valve and allow liquid to enter the chamber B. There are many valves which are controlled by oats, and it seems unnecessary therefore to illustrate such a valve in detail. Sufce it to call attention to the following United States patents which show valves of this kind:

No. 604,018, Carmichael, May 17, 1898, No.. 1,886,

468, Cornish, November 8, 1932, and Re. No. 18,253, Heath, November 1'7, 1931.

When it comes to the control of the solenoid coil |02 by opening and closing the electric circuit through conductors |03 and |04, it will be noted Athat this is done by the pan H, which is pivoted within the receiver 35 in a position to catch some of the liquid which is delivered from the bottoms of the exchange elements I0. This pan or tray H is rectangular in shape having side walls |23 and ends |24 and a. bottom |25, the latter being provided With a number of perforations |26. The pan H is carried by two arms |21, |28 which have hubs which are secured by set screws |29, |30 to a transverse shaft |3| which is journaled at its opposite ends in the side members 36, 31 of the receiver 35, at points well above the bottom of the receiver. To counter-balance the pan H, there is provided on the outer end of the shaft |3| a sleeve |32 which carries an arm |33. The sleeve |32 is secured to the shaft |3| by set screw |34. The arm |33 carries a counter-weight |35 which l is held in place upon the arm by a set screw |36.

By positioning the counter-Weight |35 at a suitable point on the arm |33, the pan H may be yieldingly held against downward movement as the liquid flows into it.

It will be seen that as the liquid flows over the elements l0, some of it will pass from each element into the tray H and if the ilow is not too heavy all of the liquid will pass out through the perforations |26. But, if the flow increases, then the liquid may notv pass through the perforations |26 as rapidly as it flows into the pan. If it does not, then the liquid will, as it were, back up and more or less ll the pan. The point atwhich this tilting of the pan will occur will depend, of course, upon the setting of the counter-weight |35. Thus, it is`clear that the pan may occupy an elevated position in which it engages a stop |31. This would be the position when there was nothing in the pan, or when the liquid flowing into the pan, passed out through the perforations |26 as fast as it came in. In suchy case there would be no backing up of the liquid to overcome the counter-balancing effect of the weight |35. The other position, however, would be that occupied by the pan when the flow of liquid was suiliciently heavy to rock the pan about its pivotal axis through shaft |3|.

The position of the pan H within the receiver 35 is indicated on the outside of the receiver by a pointer |38 which is tted upon the outer end of the shaft 3|. Preferably, this pointer is provided With a slot |39 which slips over a suitable neck near the end of the shaft, which neck has parallel sides against which the edges of the pointer on opposite sides of the slot |39 fit so as to hold the pointer against rotation except it bein response to rockings of the supporting shaft |3|. The pointer |38 consists of a plate of some length and at one end the same carries a switch box |40. The switch in the box is a mercury switch, and in'one position of,V the pan H, the switch is tilted so as to open a simple circuit and in the other position ofthe pan it closes the same circuit. 'I'hese mercury switches are well known and because of the simplicity of the one employed, it seems needless to illustrate thesame.

The switch I employ is diagrammatically represented in Fig. 1, wherein the bridging contact |4| cooperates with fixed contacts |42 and |43. As shown in this view, the normal position of the pan H leaves the circuit through the solenoid coil |02 open. In other words, while the pan H is dit empty or receiving a light ow oi' liquid, only the diaphragm 15, corresponding to the higher pressure and higher temperature, is in use. However, when the pan H is moved downward, the circuit through the solenoid coil |02 will be closed. This circuit may be traced from supply lead |44, through conductor |45, xed contact |42, bridging contact I4I, xed contact |43, conductor |03, coil |02, and conductor |04 to supply lead |46. Thus, the downward movement of the pan H closes the circuit and brings the diaphragm 16, corresponding to the lower pressure and lower temperature, into service to the exclusion of the diaphragm 15. Expressed in another way, with the pan H in its upper position, the solenoid circuit is open, the diaphragm 15 is in service, and the pressure and temperature are of high values, while with the pan H in its lowermost position, the solenoid circuit is closed, the diaphragm 16 is in service, and the pressure and temperature are of low values. With the numerical values previously mentioned as illustrative, while the diaphragm 1B is in service, the pressure of the gasified ammonia would be 43 pounds, and the corresponding temperature 28 degrees, brought into service with a heavy ilow of liquid, and, alternatively, while thediaphragm 15 is in service, the pressure would be 50 pounds, and the corresponding temperature 36 degrees, brought into service by a light ilow or non-flow of liquid.

In carrying out the invention, it will be apparent that different kinds of heat exchange elements might be employed, otheriiiquids than milk might be treated, and there might be other exchanges of heat. In some instances, it might be desirable to change from one degree of temperature to another when heating a liquid rather than when cooling it. Likewise, many changes in the details of the mechanism employed will suggest themselves to persons skilled in this art. It is therefore aimed to cover by the terms of the appended claims all of those alterations, modifications and uses which rightlyV come within the spirit and scope of the invention.

ll claim:

l. d. heat exchange systemfor use with a heat exchange medium readily vaporizable at ordinary temperatures, including a heat exchangeelement operable to bring a liquid to be treated and said medium into heat exchanging relation with each other, means for supplying said medium in liquid form to said element, means for receiving said medium from said element after it has been heated by the liquid being treated and is thereby gasified, means for delivering the liquid to be treated to-said element, means for receiving the treated liquid from said element, a regulator selectively operative according to its setting to maintain the gasied 'medium within said medium receiving means at a plurality of definite pressures, and means responsive to the amount of treated liquid passing per unit of time from the delivery point of said element to set said regulator.

2. A heat exchange system for use with a heat exchange medium readily vaporizable at ordinary temperatures, including a heat exchange element operable to bring a liquid to be treated and said medium into heat exchanging relation with each other, means for supplying said medium in liquid form to said element, means for receiving said medium from said element after it has been* heated by the liquid being treated and is thereby gasied, means for delivering the liquid to be treated to said element, means for receiving the treated liquid from said element, a compressor, a suction line extending from said medium receiving means to said compressor, a valve in said suction line, two selectively operative devices for controlling said valve, and means responsive to the amount of liquid passing per unit of time from the delivery point of said element, to operate said devices.

3. A heat exchange system for use with a heat exchange medium readily vaporizable at ordinary' temperatures, including a heat exchange element operable to bring a liquid to be'treated and said medium into heat exchanging relation with each other, means for supplying said medium in liquid form to said element, means for receiving said medium from said element after it has been heated by the liquid being treated and is thereby gasifed, means for delivering the liquid to be treated to said element, means for receiving the treated liquid from said element, a compressor, a suction line extending from said medium receiving means to said compressor, a valve in said suction line, two selectively operative devices for controlling said valve, electromagnetically actuated means for operating said devices, an operative circuit for said electromagnetically actuated means, a switch for said circuit, and a device actuated by the flow of treated liquid to operate said switch.

4. A heat exchange system for use with a heatexchange medium readily vaporizable at ordinary temperatures, including a heat exchange element operable to bring a liquid to be treated and said medium into heat exchanging relation with each other, means for supplyingr said medium in liquid form to said element, means for receiving said medium from said element after it has been heated by the liquid being treated and is thereby gasied, means for delivering the liquid to be treated to said element, means for receiving the treated liquid from said element, a compressor, a suction for operating said devices, an operative circuit for said electromagnetically actuated means, a switch for said circuit, lever means pivoted beneath said element and operative to open and close said switch, and a perforated pan carried by said lever means and lying beneath said element to catch some of the treated liquid delivered therefrom, said pan descending under a heavy flow of liquid from said element to place said switch in one operative circuit condition and rising under a light flow of liquid from said element to place said switch in another operativecircuit condition.

5. A heat exchange system including a plurality of heat exchange elements ofthe surface type adapted to occupy upright positions in substantially parallel relation to each other, means for distributing a liquid to be treated so as to flow over said elements and fall therefrom at their delivery ends, a pivotally mounted perforated tray extending beneath said elements in position to catch liquid flowing therefrom and operated by the weight of the liquid to move downward when the flow is heavy and to move upwardwhen the flow is light, means for supplying a heat exchange medium to the interiors of said elements, and means controlled by said tray movements to vary the character of said heat exchange medium.

, HARRY G. M OJONNIER. 

